BACKGROUND OF THE INVENTION
[0001] The present invention relates to a novel metallic material suitable for use as material
of constituent members of coal gasification processes and other processes in which
the constituent members are used in an atmosphere of hot gas containing sulfides.
More particularly, the invention is concerned with a sulfidation resisting Cr-Ni-Al-Si
alloy which is capable of suppressing high temperature corrosion caused by combustion
gases and other product gases.
[0002] The oil crises triggered by the Arab-Israeli war of 1973 has given rise to a demand
for developing alternative fuels as substitutes for petroleum. Among these substitute
fuels, coal is considered most significant as the basic fuel of the future because
of an abundancy of deposites as compared with petroleum. However, since the coal is
a solid fuel, it is difficult to store and transport as compared with liquid fuel.
This in turn has promoted development of techniques for converting coal into a fluid
fuel which is easy to store and transport, and also for obtaining clean energy sources
through removal of ash, SOx, etc. Typical examples of such techniques are liquefaction
and gasification of coal. The gasification of coal is a process in which coal is caused
to react with a gasifier such as oxygen, air or steam, thereby obtaining a product
gas consisting main of hydrogen, carbon monoxide, methane and so forth. Three types
of coal gasification processes have been proposed: namely, the fixed bed type, fluidized
bed type and entrained bed type. The process type, i.e., the furnace type, and the
reaction temperature'are selected in accordance with the use of the product gas.
[0003] A typical example of a furnace used for the fixed bed type process is a furnace called
a "Lurgi furnace". A large scale commercial plant of this type is operating in Sasol
in the Union of South Africa. In this process, lumps of coal of sizes ranging between
several tens of millimeters and several millimeters are fed from the top of a furnace
and are gasified while the coal is held in the form of a bed which is kept stationary.
The gasification is effected by the heat which is produced as a result of partial
burning of coal with.the aid of a gasifier which is supplied from the bottom of the
furnace. This process is advantageous in that a high thermal efficiency is obtained
by the counter-flow contact between the coal moving downwardly and the gasifier flowing
upwardly, but suffers from various disadvantages such as generation of tar in the
low temperature region due to a large temperature gradient in the furnace. In addition,
this process cannot be applied to the processing of powdered coal and caking coal,
and the processing rate is impractically small.
[0004] The fluidized bed type process and the entrained bed type process do not suffer from
the disadvantage of the fixed bed type process, and are also capable of treating the
remnant of crude oil which has to be utilized. For these reasons, intense study and
development of these types of coal gasification process are being vigorously undertaken,
particularly in U. S. A. and West Germany. In the fluidized bed type pr6cess, powdered
coal of particle sizes falling within a predetermined range of between several millimeters
and several hundreds of microns are charged into a gasification furnace. The powdered
coals are fluidized and gasified by a gasifier which is also blown into the furnace.
By virtue of the use of powdered coals, this process exhibits a superior heat conduction
through convection, so that the reaction takes place uniformly, thus reducing the
tendency for tar to be generated as a byproduct. The disadvantage of this type of
coal gasification process is that the coal used in this process has to have such a
particle size that adequate fluidity of the coal is maintained.
[0005] The entrained bed type process is a process in which pulverized coal of particle
sizes ranging between several tens of microns and several hundreds of microns is blown
into the furnace from the bottom and is gasified at a high temperature. This process
can gasify any type of coal without requiring mechanical stirring or pre-treatment,
and is able to gasify the coal almost completely without generation of tar. This process,
however, requires pulverization of the coal, and difficulty is experienced in controlling
the residence period of the coal in the furnace, as well as in connection with certain
problems concerning the system such as facilities for discharge of slag and utilization
of sensible heat.
[0006] The metallic materials used in coal gasification furnaces are inevitably subjected
to high temperature as a result of burning of the coal, unlike the material used in
coal liquefaction systems. This imposes a problem of corrosion of the metallic materials
by hot gases such as CO, C0
2, H
2, H
2S and CH
4 which are generated as a result of burning of the coal. In particular, H
2S at high temperature causes heavy corrosion which is usually referred to as sulfur
attack.
[0007] In order to put the developed process into practical use on a greater scale, it is
necessary to construct a highly reliable plant through development of economical materials
or working techniques which enable the constituent elements of the furnace to withstand
severe conditions in the gasification process. Thus, the constituent metallic materials
used in coal gasification plants are required to withstand the hot corrosive coal
gases to which they will be exposed, particularly H
2S which causes serious sulfur attack.
[0008] Among various austenitic steels proposed hitherto, AISI 304 (18Cr-8Ni steel), AISI
316 (l8Cr-8Ni-Mo steel), AISI 321 (18Cr-8Ni-Ti steel) and AISI 347 (l8Cr-8Ni-Nb steel)
are used broadly as the constituent materials for various plants by virtue of their
high- temperature strength and workability, as well as low cost and the ease with
which they can be manufactured. The use of these austenitic steels is spreading also
to the field of piping in nuclear plants and boilers, as a result of improvements
in anti-stress corrosion cracking sensitivity through reduction of C content and improvements
in anti-steam corrosion properties by refining of the crystal grains. Using these
materials for which the easiness of production and other properties are known is advantageous
from the viewpoints of design, cost and reliability.
[0009] These austenitic stainless steels, however, exhibits serious corrosion degradation
due to corrosion by gases at high temperatures, particularly grain boundary attack
by sulfides.
[0010] It has been proposed that the anti-corrosion properties at high temperature may be
improved by increasing the Cr content. Examples of materials having increased Cr content
are: AISI 309S (2lCr-l3Ni steel), AISI 3108 (25Cr-20Ni steel), Incoloy 800 (2lCr-32Ni-Ti,
Al steel), Inconel 671 (50Cr-50Ni steel) and so forth. These materials have been proposed
in view of the fact that inclusion of at least 20 to 25
% of Cr is necessary for attaining high corrosion resistance of materials in long use.
Attention has been given to these materials because of their easiness of manufacture
and good workability, but the improvement in their resistance to corrosion by sulfides
such as H
2S is still unsatisfactory due to the fact that the Ni content is necessarily increased
in correspondence with the increase in the Cr content in order to maintain the workability
and austenitic structure.
[0011] Under these circumstances, there is an increasing demand for development of an inexpensive
mater.ial easy to produce and having high workability, as well as high corrosion resistance
equivalent to that of AISI 309S, AISI 310S and Incoloy 800.
SUMMARY OF THE INVENTION
[0012] Accordingly, an object of the invention is to provide an alloy steel which exhibits
high anti-sulfur attack property in an atmosphere of hot coal gas.
[0013] Through intense study and experiments on the materials which can be used for of structures
to be employed in coal gasification processes, the present inventors have found that
the grain boundary corrosion caused by sulfides can be suppressed in ordinarily used
austenitic steel materials such as AISI 304, AISI 316, AISI 321 and AISI 347 if a
suitable amount of Si is added besides Al to these austenitic steels. Such austenitic
steels containing Si and Al in combination have proved to exhibit superior corrosion
resistance in - a coal gas atmosphere, i.e., high resistance to grain boundary corrosion
by sulfides at high temperatures, and are therefore better suited for use as the structural
materials employed in coal gasification plants than known austenitic steels such as
AISI 309S, AISI 310S and Incoloy 800.
[0014] According to the invention, there is provided a structural member to be subjected
to a hot gas atmosphere produced through reaction between coal and a gasifier such
as oxygen, air, steam or hydrogen, the structural member being made of an anti-sulfur
attack Cr-Ni-Al-Si alloy steel which is prepared as follows.
[0015] Namely, the alloy steel in accordance with the invention can be obtained from one
of the following four types of steels: namely, a steel containing, by weight, not
greater than 2% of Mn, 8 to 11% of Ni and 18 to 20% of Cr; a steel containing not
greater than 2.0% of Mn, 10 to 14% of Ni, 16 to 18
% of Cr and 2 to 3% of Mo; a steel containing not greater than 2.0% of Mn, 9 to 13%
of Ni, 17 to 20% of Cr and not greater than 0.6% of Ti; and a steel containing not
greater than 2.0% of Mn, 9 to 13
% of Ni, 17 to 20% of Cr and not greater than 1% of
Nb +
Ta. In one of these steels, the C content is increased to 0.03 to 0.3%, and 0.5 to
10% of Al and 1 to 10
% of Si are added in combination, such that the balance is constituted by not less
than 50% of Fe.
[0016] The alloy steel in accordance with the invention exhibits a remarkable gas corrosion
resistance at high temperatures, when used in a coal gas atmosphere generated in a
coal gasification process in which a product gas consisting mainly of hydrogen, carbon
monoxide and methane is produced through reaction between coal and a gasifier such
as oxygen, air, steam and so forth.
[0017] In case of the 18% Cr-8% Ni austenitic stainless steel, the gas corrosibn resistance
at high temperatures was significantly improved by the addition of a suitable amount
of Al followed by addition of Si, even when the C content was increased to range between
0.03 and 0.3%. Steels having large Al and Si contents are rather inferior in workability.
Therefore, the constituent member which requires a high workability of the material
is formed by forging or rolling from an alloy steel which has comparatively small
Al and Si contents, whereas the constituent member in which preference is given first
to the corrosion resistance rather than workability is made by casting from an alloy
steel having large Al and Si contents. It has thus been proved that various constituent
members for use in coal gasification process can be obtained by suitably selecting
the Al and Si contents of the alloy steel, without impairing the functions required
for such members.
[0018] The reasons for limitation of content in respect of each alloy element in the alloy
steel of the invention will be described hereinunder.
[0019] C: C is an important element because it serves as an austenite former and because
it ensures a high ! strength at high temperatures. In order to permit the addition
of Al and Si and to stabilize the structure as much as possible without impairing
the corrosion resistance, the C content preferably ranges between 0.03 and 0.3%, more
preferably between 0.07 and 0.15%.
[0020] Si: Si is a significant element for attaining the properties required for the alloy
steel of the invention. For obtaining a high corrosion resistance, the Si content
should be not smaller than 1%. Addition of-Si in excess of 10
%, however, causes saturation in the effect of improvement in corrosion resistance,
and undesirably impairs the workability and the castability.
[0021] The effect produced by the addition of Al varies according to the amount of addition
of Al. When Si is added alone, no substantial improvement in the corrosion resistance
is achieved when the Si content is not greater than 1.0
%, and Si content should not be smaller than 2.0% if an appreciable effect is to be
obtained. A greater effect is produced when Si is added in combination with Al than
when it is added alone. The Si content preferably ranges between 3 and 5
%.
[0022] Mn: Mn serves as an austenite former but the Mn content is preferably relatively
small because Mn tends to impair the oxidation resistance. For this reason, the Mn
content is selected to be not smaller than 2%, preferably between 1 and 2
%.
[0023] Ni: Ni is one of the basic constituent elements of austenitic stainless steel. The
Ni content should be not smaller than 8%, in order to maintain an austenite structure
in spite of the addition of Al and Si which are ferrite formers. Addition of Ni in
excess of 14
% impairs the resistance to sulfur attack in a coal gas atmosphere.
[0024] Cr: This element is the most fundamental element for improving the gas corrosion
resistance at high temperatures. The Cr content should be 16
% or greater but is limited to be not greater than 20
% in view of the Ni content.
[0025] Ti, Mo, Nb: Ti, Mo and Nb are elements which are effective in improving the high
temperature strength through formation of safe carbides and nitrides. In order to
obtain an appreciable effect, Ti, Mo and Nb content should be so selected as to be
not greater than 0.6%, 2 to 3% and not greater than 1%, respectively.
[0026] Preferably, Ti content and Nb content should range between 0.2 and 0.5%, respectively.
[0027] Al:
Al is an important element which provides, in cooperation with Si, a superior anti-sulfur
attack property. The Al content ranges between 0.5 and 10
%, preferably between 2 and 5%. This element improves the gas corrosion resistance
at high temperatures even when it is added alone to the austenite stainless steel.
The effect is further increased, however, when Al is added together with Si. In order
to attain an appreciable effect, the Al content should not be less than 0.5%. Addition
of Al in excess of 10
% causes saturation in the improving effect and, instead, causes problems in workability
and castability. For this reason, the Al content is limited to be not greater than
10%. When the need for workability is not so strict, an Al content ranging between
2 and 5% provides satisfactory corrosion resistance. When the material is to be forged,
the Al content can be increased up to 10%.
[0028] The alloy steel in accordance with the invention can contain other elements which
are inevitable included in the course of production, besides the elements mentioned
hereinabove.
[0029] In some cases, the knowledge concerning the contents of elements as specified above
may prove insufficient for the practice production of an alloy steel in accordance
with the invention. There is also a risk that the alloy steel of the invention will
become cracked during subsequent working. In order to obtain a material having practical
utility, therefore, it is necessary to suitably adjust the contents of the alloy elements
in relation to each other.
[0030] More specifically, when Al is added alone, the material can be formed into sheets,
bars and pipes, regardless of whether the work is done in a hot or cold state, provided
that the Al content is not greater than 5
%. However, an Al content exceeding 5% causes a risk of cracking during working. Addition
of Si by an amount equal to the amount of Al causes a more serious effect on workability
than in the case where Al is added alone. When Si is added together with Al, therefore,
it is necessary to effect an adjustment of the alloy elements by increasing the C
content, while suppressing the Ni and Cr contents, or to use the material as it is
after casting. Such an adjustment of the properties of alloy elements facilitates
the application of the material of the invention to equipment and members which are
subjected to gas atmosphere containing sulfides produced in coal gasification systems,
e.g., the water-cooled wall tube of a coal gasification furnace, the constituent members
of a heat exchanger, valves, nozzles and so forth.
[0031] Briefly, the material in accordance with the invention is an anti-sulfur attack Cr-Ni-Al-Si
alloy which has an improved resistance to the grain boundary corrosion which is caused
by hot gas produced as a result of reaction between coal and a gasifier such as. oxygen,
air and steam, particularly resistance to grain boundary sulfur attack by sulfides
in such hot gas. The composition of the material in accordance with the invention
contains: 0.03 to 0.3% of Cl; not greater than 2
% of
Mn;
Ni, Cr, Mo, Ti and Nb in amounts falling within the ranges of austenitic stainless
steels AISI 304, AISI 316, AISI 321 and AISI 347; 0.5.to 10
% of Al in combination with 1 to 10% of Si; and the balance substantially Fe and impurities
inevitably included during production.
[0032] The invention will be described hereinunder with reference to the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0033]
Fig. 1 is a schematic illustration of a coal gasification system;
Fig. 2 is a graph showing the relationship between Al content of the alloy steel and
the corrosion loss;
Fig. 3 is a graph showing the relationship between Si content of the steel and the
corrosion loss;
Fig. 4 is a block diagram of a coal-gasification power-generating composite plant
having a coal gasification system which employs structural members of the invention;
Fig. 5 is a schematic vertical sectional view of a jet bed type gasification furnace;
and
Fig. 6 is a sectional view taken along the line VI-VI of Fig. 5, showing the heat
collecting zone in the upper part of the gasification furnace.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0034] Table 1 shows the chemical compositions of examples of alloy steels in accordance
with the invention, together with comparison steels. The contents of elements in this
Table are shown in terms of weight percent. In each steel, the balance is substantially
Fe and inevitable impurities such as P, S, etc. The sample Nos. 1 to 18 are alloy
steels in accordance with the invention, while sample Nos. 26 to 30 are comparison
steels. These samples were prepared by vacuum-melting and casting the materials, followed
by 1-hour water cooling at 1100°C. Test pieces of 6 mm x 20 mm x 25 mm were prepared
from them. Sample Nos. 19 to 25 are forged materials. The test pieces of the sample
Nos. 19 to 25 were prepared after 30 minutes of heating at l100°C and subsequent water
cooling, while the test pieces of sample Nos. 24 and 25 were formed after 30 minutes
of water cooling at 1150°C and subsequent water cooling.

[0035] These test pieces were subjected to a corrosion test in which they were held for
100 hours within an atmosphere simulating a coal gas, containing 24
% of H
2, 18% of CO, 12% of CO
2, 6% of CH
4, 0.5% of H
2S and the balance H
20. The test temperature was 850°C, while the temperature was 30 ata. The corrosion
loss is expressed in terms of the sum of reduction in thickness and depth of corrosion
(grain boundary corrosion). The results of the test are shown in Table 2.

[0036] As will be understood from Table 2, the alloy steel of the invention exhibits a remarkably
improved resistance to corrosion by gas at high temperature as compared with comparison
steel Nos. 19 (AISI 304), 20 (AISI 316), 21 (AISI 321) and 22 (AISI 347). In particular,
the alloy steel sample Nos. 7 to 10 of the invention, to which Si is added together
with 20% of Al, exhibit superior corrosion resistance even over the comparison steel
sample Nos. 24 (AISI 310 S) and 25 (Incoloy 800) which have large Cr contents and,
hence, exhibit high corrosion resistance. It will be understood also that, when the
Al content is the same, higher corrosion resistance can be obtained by addition of
not less than 1.5% of Si, as in the case of alloy steel sample Nos. 1 to 5 and 12
in comparison with comparison steel No. 23 (SUS 631) and comparison steel Nos. 26
to 30.
[0037] Fig. 2 shows the relationship between the Al content and the corrosion loss in the
alloy steel of the invention to which 2
% of Si is added together with Al, in comparison with that of the comparison steels
to which Al is added alone. It will be seen that the corrosion resistance is improved
by the combined inclusion of Al and Si as compared with the case where Al is added
alone.
[0038] Fig. 3 shows a relationship between the Si content and the corrosion loss, in alloy
steels to which Si has been added in various amounts in addition to 2
% Al. It will be understood from this Figure that the resistance to corrosion by hotgas
is increased by increase in the Si content, as compared with the case where Al is
added alone, and also that the Si content should be not smaller than 1.5% in order
to obtain an appreciable effect.
[0039] As explained before, the alloy steel in accordance with the invention is effectively
used as materials of devices and members which are subjected to an atmosphere containing
sulfides produced in a coal gasification system, e.g., a water-cooled tube wall of
a gasification furnace, members of a heat exchanger, valves, nozzles and so forth.
A coal-gasification combined cycle power plant, which employs such a coal gasification
system, will be explained hereinunder by way of example.
[0040] Fig. 4 is a block diagram of a coal-gasification combined cycle power plant which
has various parts made from the material in accordance with the invention. Fig.5 is
a schematic vertical sectional view of a entrained bed type coal gasification furnace,
while Fig. 6 is a sectional view taken along the line VI-VI of Fig. 5, showing an
upper water-cooled structure of the gasification furnace.
[0041] Coal 1 is introduced by means of a burner 3 into a gasification furnace 4 to which
also introduced is oxygen as a gasifier 2. The coal 1 thus introduced is gasified
in a gasification zone 5. The gasification zone 5 is defined by a refractory structure
6 because a high temperature exceeding 1600°C is established in the gasification zone.
The coal gas of high temperature is delivered to a heat collecting zone 8 which is
constituted by a water-cooled structure 17 made from an alloy steel of the invention
and is cooled down below 900°C before it reaches the outlet of the gasification .furnace
4. The gas as a crude gas 10 coming from the outlet of the gasification furnace 4
is sent to a steam generator 11 which is made of an alloy steel in accordance with
the invention, so that the crude gas 10 is cooled through a heat exchange in the steam
generator 11. Thus, the sensible heat posessed by the crude gas 10 is collected as
the energy of
"steam 12. The crude gas 13 coming out of the steam generator 11 is sent to a gas-gas
heat exchanger 14 which is made of an alloy steel in accordance with the invention,
where heat is exchanged between the crude gas 13 and the refined gas 15, so that the
crude gas is cooled down to the temperature suitable for the refining before it is
sent to a gas refining section 16. The gas 15 refined in the gas refining section
16 makes a heat exchange with the crude gas in the gas-gas heat exchanger such as
to be heated by the crude gas, and is supplied as a fuel gas 18 to a gas turbine combustor
19. The hot combustion gas expands through a gas turbine to drive a generator, thereby
generating electric energy.
[0042] This composite plant has a heat recovery system which will be explained hereinunder.
The exhaust gas 20 exhausted from the gas turbine is introduced into a heat recovery
boiler 22 such as to produce a sensible heat of steam 12. On the other hand, the crude
gas 10 available at the outlet of the gasification furnace 4 delivers sensible heat
to water in the steam generator .11.The steam 12 generated in the heat recovery boiler
22 and the steam 12 generated in the steam generator 11 merge in each other and the
thus mixed steam is superheated in , a superheater such as to become superheated steam
which is sent to a steam turbine 23. The superheated steam expands through the steam
turbine 23 which in turn drives a generator thereby generating electric energy. The
steam discharged from the steam turbine 23 is condensed in a condenser 24 to become
condensate which in turn is fed as feedwater to the heat recovery boiler 22 by a feedwater
pump.